CN209501648U - A kind of heat chemistry modified technique system - Google Patents
A kind of heat chemistry modified technique system Download PDFInfo
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- CN209501648U CN209501648U CN201822142309.0U CN201822142309U CN209501648U CN 209501648 U CN209501648 U CN 209501648U CN 201822142309 U CN201822142309 U CN 201822142309U CN 209501648 U CN209501648 U CN 209501648U
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- pipe
- mixer
- tank
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- pipeline
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Abstract
The utility model discloses a kind of heat chemistry modified technique systems, including adjusting tank, reaction kettle, discharge tower, pressurized canister, alkali liquid tank, acid solution tank, grug feeding jar, heat exchanger, first pipe mixer, second pipe mixer and third pipe-line mixer, the feed end of first pipe mixer is connect with adjusting tank and alkali liquid tank by pipeline, first pipe mixer is connect by heat exchanger with reaction kettle, reaction kettle is connect by energy converter with discharge tower, discharge tower by pipeline successively with second pipe mixer, third pipe-line mixer is connected with pressurized canister, second pipe mixer is connect by pipeline with grug feeding jar, third pipe-line mixer is connect by pipeline with acid solution tank；By heat exchanger after being reacted after the heat chemistry modified technique system lye is mixed with adjusting liquid and into reactor tank, so that heat is fully utilized, improve the utilization rate of heat.
Description
Technical field
The utility model relates to a kind of heat chemistry modified technique systems.
Background technique
In the modern times, due to the progress of science and technology, calorimetric method is improved, the especially raising of thermal measurement precision,
Heat chemistry still has significance in the fields such as fuel, food and biology and drug.(such as combustion heat generates thermochemical data
Heat etc.) calculation of thermodynamics, engineering design and in terms of all have a wide range of applications.The modified work of existing heat chemistry
Process system only carries out heat exchange by heat exchanger after reactor tank reaction, and heat utilization ratio is low.
Utility model content
Purpose of the utility model is to solve defects in the prior art, provide a kind of utilization rate of raising heat
Heat chemistry modified technique system, to solve problems of the prior art.
To achieve the above object, the technical solution of the utility model is as follows:
A kind of heat chemistry modified technique system, including adjust tank, reaction kettle, discharge tower, pressurized canister, alkali liquid tank, acid solution tank,
Grug feeding jar, heat exchanger, first pipe mixer, second pipe mixer and third pipe-line mixer, the first pipe mixing
The feed end of device is connect with adjusting tank and alkali liquid tank by pipeline, in the pipeline between the first pipe mixer and alkali liquid tank
Be provided with lye pump, the first pipe mixer is connect by heat exchanger with reaction kettle, the first pipe mixer with change
Reaction kettle feed pump is provided between hot device, the reaction kettle is connect by heat exchanger with discharge tower, and the discharge tower passes through pipe
Road is successively connect with second pipe mixer, third pipe-line mixer and pressurized canister, and the second pipe mixer passes through pipeline
It is connect with grug feeding jar, dosing pump, the third pipeline is provided on the pipeline between the second pipe mixer and grug feeding jar
Mixer is connect by pipeline with acid solution tank, is provided with acid solution on the pipeline between the third pipe-line mixer and acid solution tank
Pump.
In order to further realize the utility model, the adjusting tank is connected with flue gas leading.
In order to further realize the utility model, the reaction kettle is connect with adjusting tank by the first reflux line.
In order to further realize the utility model, the discharge tower is connect with adjusting tank by the second reflux line.
Beneficial effect
By exchanging heat after being reacted after the heat chemistry modified technique system lye is mixed with adjusting liquid and into reactor tank
Device makes heat be fully utilized, and improves the utilization rate of heat；In addition, reaction kettle and adjusting tank pass through the first reflux line
Connection, discharge tower are connect by the second reflux line with adjusting tank, recycle, economize on resources to the gas of volatilization.
Detailed description of the invention
Fig. 1 is the structural block diagram of the utility model heat chemistry modified technique system；
Description of symbols:
1, tank is adjusted；2, reaction kettle；3, discharge tower；4, pressurized canister；5, alkali liquid tank；6, acid solution tank；7, grug feeding jar；8, it changes
Hot device；9, first pipe mixer；10, second pipe mixer；11, third pipe-line mixer；12, flue gas leading；13, lye
Pump；14, the first reflux line；15, the second reflux line；16, dosing pump；17, acid pump；18, compressed air pipe；19, anti-
Answer kettle feed pump.
Specific embodiment
The utility model is further described in detail with reference to the accompanying drawing, these attached drawings are simplified signal
Figure, only illustrates the basic structure of the utility model, the direction of this specific implementation is using the direction Fig. 1 as standard in a schematic way.
Embodiment one
As shown in Figure 1, the utility model heat chemistry modified technique system includes adjusting tank 1, reaction kettle 2, discharge tower 3, adding
Press tank 4, alkali liquid tank 5, acid solution tank 6, grug feeding jar 7, heat exchanger 8, first pipe mixer 9, second pipe mixer 10 and third
Pipe-line mixer 11, in which:
The feed end of first pipe mixer 9 is connect with adjusting tank 1 and alkali liquid tank 5 by pipeline, is adjusted tank 1 and is connected with
Flue gas leading 12 is provided with lye pump 13 for exhaust gas to be discharged in the pipeline between first pipe mixer 9 and alkali liquid tank 5, and first
Pipe-line mixer 9 is connect by heat exchanger 8 with reaction kettle 2, is provided with reaction kettle between first pipe mixer 9 and heat exchanger 8
Feed pump 19, reaction kettle 2 are connect by heat exchanger 8 with discharge tower 3, and reaction kettle 2 and adjusting tank 1 pass through the first reflux line 14 and connect
It connects, discharge tower 3 is connect with adjusting tank 1 by the second reflux line 15, and discharge tower 3 is successively mixed with second pipe by pipeline
Device 10, third pipe-line mixer 11 and pressurized canister 4 connect, and second pipe mixer 10 is connect by pipeline with grug feeding jar 7,
Dosing pump 16, third pipe-line mixer 11 are provided on pipeline between second pipe mixer 10 and grug feeding jar 7
It is connect by pipeline with acid solution tank 6, acid pump 17 is provided on the pipeline between third pipe-line mixer 11 and acid solution tank 6, is added
Pressure tank 4, which is connected in 18 pairs of pipes of compressed air pipe, to pressurize, and the outlet of pressurized canister 4 is connected to filter press.
By exchanging heat after being reacted after the heat chemistry modified technique system lye is mixed with adjusting liquid and into reactor tank
Device makes heat be fully utilized, and improves the utilization rate of heat；In addition, reaction kettle and adjusting tank pass through the first reflux line
Connection, discharge tower are connect by the second reflux line with adjusting tank, recycle, economize on resources to the gas of volatilization.
The foregoing is merely the better embodiment of the utility model, the utility model is not limited to above-mentioned embodiment party
Formula, there may be the structural modifications that part is small in implementation process, if various changes or modifications to the utility model are not
The spirit and scope of the utility model are detached from, and are belonged within the scope of the claims and equivalents of the utility model, then originally
Utility model is also intended to encompass these modification and variations.
Claims (4)
1. a kind of heat chemistry modified technique system, which is characterized in that including adjusting tank, reaction kettle, discharge tower, pressurized canister, lye
Tank, acid solution tank, grug feeding jar, heat exchanger, first pipe mixer, second pipe mixer and third pipe-line mixer, described
The feed end of one pipe-line mixer with adjust tank and alkali liquid tank and connect by pipeline, the first pipe mixer and alkali liquid tank it
Between pipeline in be provided with lye pump, the first pipe mixer is connect by heat exchanger with reaction kettle, the first pipe
Reaction kettle feed pump is provided between mixer and heat exchanger, the reaction kettle is connect by heat exchanger with discharge tower, described to release
Pressure tower is successively connect with second pipe mixer, third pipe-line mixer and pressurized canister by pipeline, the second pipe mixing
Device is connect by pipeline with grug feeding jar, is provided with dosing pump on the pipeline between the second pipe mixer and grug feeding jar, institute
It states third pipe-line mixer to connect by pipeline with acid solution tank, be set on the pipeline between the third pipe-line mixer and acid solution tank
It is equipped with acid pump.
2. heat chemistry modified technique system according to claim 1, which is characterized in that the adjusting tank is connected with exhaust gas
Pipe.
3. heat chemistry modified technique system according to claim 1, which is characterized in that the reaction kettle passes through with tank is adjusted
The connection of first reflux line.
4. heat chemistry modified technique system according to claim 1, which is characterized in that the discharge tower passes through with tank is adjusted
The connection of second reflux line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822142309.0U CN209501648U (en) | 2018-12-20 | 2018-12-20 | A kind of heat chemistry modified technique system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822142309.0U CN209501648U (en) | 2018-12-20 | 2018-12-20 | A kind of heat chemistry modified technique system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209501648U true CN209501648U (en) | 2019-10-18 |
Family
ID=68195774
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822142309.0U Expired - Fee Related CN209501648U (en) | 2018-12-20 | 2018-12-20 | A kind of heat chemistry modified technique system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209501648U (en) |
-
2018
- 2018-12-20 CN CN201822142309.0U patent/CN209501648U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191018 Termination date: 20201220 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |